Temperaturreglering av formspruta

Image Processing Techniques for Ash Line Detection

For efficient firing in sloping grate bark ovens, it is important to control the ash line position on the grate. Here, the problem of detecting the ash line with an image processing system is treated. The presentation of trend curves to the operator is of special interest. The trend curves shall indicate how the ash line position changes with time, and in that way improve the manual control of the

Laborationsserie i reglerteknik för Asea Novatune

This is a presentation of automatic control theory in combination with an introduction to the digital controller Asea Novatune. The work is done as part of a master degree in science at Lund Institute of Technology, Department of Automatic Control, with Asea Innovation, Västerås, as sponsoring organization. The presentation is to be used within Asea Innovation for education. The presentation has

Temperaturreglering vid värmebehandling av elakartade tumörer

Simulering av en reaktionskalorimeter

Rörelsedetektering i bildsekvenser

Demonstrationssystem för Asea Master

Simulering av en hybrid självinställande regulator

Bestämning av parametrar i dämptillsats för dämpning av effektpendlingar i kraftnät

En auto-tuner för PI regulatorer

Reglerpaket för digital reglering med dödtidskompensering och framkoppling

System med svagt dämpade poler

Temperaturreglering, hjärt-lung maskin

Loggningsprogram for $\mu$-Mac 5000

Konstruktion av en robotarm med adaptiv reglering

En drivrutin för kommunikation mellan Onspec och Cluster controller

Experiments with User Interface for Computer Aided Control Engineering

Datorsimulering av diskreta förlopp i torpedtuber

Syresättning av gluconobacter oxidans

Infrysning av livsmedel - Simulering av en industriell process

Design and operation of industrial freezers contains the crucial problem of how to make the frozen foods attain a prescribed temperature. Methods for prediction of freezing times under given constant conditions are commonly used in order to calculate the optimum product flow through continuous freezers. However, in reality the processes are time variable, due to disturbances and parameter deviatio